Page 276 - Pressure Swing Adsorption
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 252   PRE.5SURE SWING ADSORPTION   PSA PROCE.5SE.5                   253

 The basic orinciole of a  PSA "concentration process"  may be understood   In  the limtt of Yo->  0 and  /3  ->  0 (high  seiect1v1tv)  these exoresstons reduce
 from  eouilibnum  theory  (see  Section  4.2  and  Figure  4.25).  Consider  an   to:
 adsorbent  bed  equilibrated  at  pressure  P and  mole  fraction  (of the  more
 O
 strongly adsorbed species)  y •  If the euuilibna are linear:     (6.12)
 0
 .   p   p
 q~  ~ KAcA  ~ KAy RT'   q; ~ K 8c 8  ~ K 8 (1  - Y) RT   (6.3)
                      I  I  \
 By combining the differential mass balance exoress1ons for both components   F  =B!n\..0'.<>.J
                         - y
               A
                   •
                        ]
 (Ea. 4.4), we  obtam:
 _!__  ap  + {._!__  _  _!__) a(Py)  +  a(Pv)  ~   ( .4)
 /3 at   \/3A   [3 8   at   ·  az   0   6
 8
            Figure  6.21  shows  FA  and  F  plotted  agamst  the  pressure  ratio  for
 and by  elimmatmg the term av /az  between Eqs. 4.4 and 6.3:   8
         different values of  y •  The cmves  are  nonlinear, but, when  the selecttv1ty  1s
                          0
 ay)   f3Av   (ay)   (/3-1)(1-y)y dlnP
 (  iii  ,  +  1 + ( f3  - 1) y  az  ,   1 + ( /3  - 1) y   dt   ( 6.5)
 m  which  /J  =  BA/(3 8   and  the  total  pressure  differential  anses  from  the
 assumption  of negligible pressure  drop  across  the coiumn  [P =  P(t )].  Since
 y  ~ y(z, t), the left-hand side of Ea. 6.5  is s1moly  the total lime derival!ve of
 y, and the variatioff of comoosition during pressurization or blowdown  steps
 1s  given  by  Ea.  4.8.  It  follows  by  direct  mtegration  that  the  vanat10n  m   ~ 0 0,0!
                                        V  0.0!
                                         0
 composition  during pressurization  or blowdown will  be given by:   0
 l'...  - (...:...=1'...)µ(.!!_)µ-,   (6.6)
 Yo  -  J  - Yo   _ Po
 Eouations 4.4  and 6.4 yield:
 _i ap  + (/3  _  /(vPy)  + a(vP)  ~
 f3a  at   1  az   az   0   (6.7)
 Neglecting the axial variat10n of pressure leaves only the time dependence; so
 the  velocity  durmg a  pressurization or blowdown  step can  be  found  simply
                       0.8
 mtegratmg from  the closed end:
 -z   d In P
 (6.8)               8
 '' =  f3n[I  + (/3- l)y]   dt   00   0.6
                     iii
 The  fraction  of  A  desorbed  durjng  blowdown  from  pressure  1' to  P  is   ~
 0
 given  by:          i':i
                     r
                    u  <   0. 4
 F  ~ f PB  vyPdt   (6.9)   ~
                    ~
 A   AZ)'  p
 P  O  O
 0
 and subsl!tutmg for  v  and  y  from  Eqs. 6.8 and 6.6:   0.2
 /3   (·l-yo\µ;cp-1)  p   y'l<P-1)   .              A  y 0.0!
                                                         0
 I
 FA  - l  - 8  ~  t (1  - y/2"-ll/(p-1) dy   ( 6.10)   0   ·,
                                0.8     0,S    0,4    0.2
 Similarly, for the  fraction of B  desorbed:
                                           PIP  .
 I   (   Yo  )1;<1-plf Po  y(2-.B)/<.B-n
 F  =-.- --  ~---~dy   ( 6.11)
 8   I - /3  1 - Yo   P  ( 1 - y t1<a- 1l   Figure 6.21  Fractional desorption durmg blowdown for differeni combinat1ons of Yo
         and fl, calculated according to Eos.  6.10 anct  6.1).
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